US1880534A - Production of hydroquinone - Google Patents

Description

Oct. 4, 1932. H. voN BRAMER l-:T AL 1,880,534

PRODUCTION 0F, HYDRQQUINONE Filed May 17. 1929 mwa? s w PREHEATER,

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UNITED STATES v.lnfrrzla'lv OFFICE HAROLD VON BEAMER AND JOHN ZABRISKIE, .OF PASSAIC JUNCTION, NEW JERSEY,

ASSIGNORS T EASTMAN KODAK COMPANY, OF ROCHESTER, NEW YORKNA. CORPO- RATION ,OF YORK PRODUCTION OF HYDROQUINONE Application led Hay 17,

This invention relates to the production of4 hydroquinone and more particularly to the separation of quinone resulting from the oxidation of aniline and the reduction of the quinone so producedto hydroquinone.

Heretofore, the method usually employed for the production ofhydroquinone has been a two-batch method involving (l) the oxida- C tion of aniline to quinone by theI use of manmultiplicity of steps. It was found by us, by

actual practice, that the employment of'the above method was tedious and time consuming, requiring approximately seven days to complete all steps thereof; we also found that it was impossible to obtain thereby more than approximately `an 80% yield.

We have discovered that following the oxidation of the aniline to quinone, the quinone can be vaporized from the reaction mixture by the employment of steamv distillation, not in the manner which would ordinarily be expected, namely, by blowing the steam through the reaction mixture, but by steam distilling the quinone from the reaction jmixture in a tower subject to the.` conditions hereinafter set forth. While in the vapor state the quinone and steam are conducted immediately to an Y .eductor which intimately mixes the' quinone vapor with a recirculatedlcurrent of water and suspended iron dust, thereby reducing the quinone to hydroquinone,

Various attempts have been made in the past to separate quinone from the reaction mixture by'steam distillation but all, so far 'as our information goes, have been unsuccessful for the reason that the instant that quinone in solution is subjected to steam distillation it quite readily decomposes into undesirable elements.V This has resulted. in the practice 1929. Serial N0. 363,808.

heretofore of conducting the reducing reaction in the same reaction mixture as that in which the quinone was formed.

Rather opposed to the conclusions of those who have previously worked with these materials, we iind .that if the reactionV mixture containing quinone is very rapidly preheated to the temperature of 1o.w pressure steam, the quinone can be vaporized from the reaction mixture by the useofsteam without the decomposition of thefquinone. As a further condition to our methdd of steam distillation, we also have found it'quite desirable to spray or otherwise diffuse thfquinone reaction mixture into a tower containing coke or otherv suitable material for physically breaking up the quinone reactionl mixture so as to obtain a rapid and intimate contact between the steam and thel reaction mixture for the vapo'rj ization of the quinone therefrom.

As a further step in our invention, we then conduct the mixture of quinone and steam va-V por, without exposure to air, to the eductor above referred to. This eduction apparatus includes means for continually recirculating a suspension of iron dust in water through an eductor nozzle which, by virtue of its aspirator effect, sucks into the stream of water andv -iron dust the quinone and steam vapors. By

such an. arrangement, a very intimatejcontact ofthe quinone with the iron dust in water is obtained so that practicallyan immediate reaction' takes place by which the quinone is reduced to hydroquinone. To insure ycompletion of the reaction, the quinone vapors (if any there be, which pass the eductor nozzle without being completely reacted) are permitted to travel through a pipe of some length through which the water and iron dust are being circulated in order that com-v v pletion of the reaction may be assured. By

is reacted upon. The vat temperature of the hydroquinone solution is maintained at approximately-Q". to 97o C., although due to the eduction of steam into thev recirculation stream, the temperature at which the reduction reaction is permitted to take place is substantially 100 C.

When all of the quinone has been reduced to hydroquinone, all that remains to be done is to filter the solution of hydroquinone so as to remove the iron products therein andv allow the hydroquinone to crystallize from the solution, thereafter drying the crystals in a well known manner. We have found that by our improved method we have been able to obtain a product with a purity as high as 95% or even greater, and that the process may be tuting a part hereof and in which is illusv.trated a steam acketed tower 1, packed with coke or other suitable packing which has a test outlet 2 and is mounted upon and in communication with a still or kettle 3 which is provided withboth direct and indirect steam. A. short pipe 4 leads from the top of the tower 1 to the eductor 5. A small vertical line Gjconnects the eductor with the tank 7 which is provided with "a return or recirculation line 8 g having a pump `9 in series therewith to provide for the recirculation of the water and iron dust mixture through the eductor 5. The oxidation of the aniline to quinone may be conducted in the vat or tank 11 in which the reaction mixture containing the quinone is continually agitated by means of the stirrer 12. A pump 13 and recirculation line 14 are also provided for reeirculating thequinone reaction mixture, the line 14 being provided 'with a take-offline 15 controlled by a valve 16 which permits a constantflow ofthe quinone reaction mixture to pass into the preheater 17. It will be noted that theline 4 is sloping and that the quinone reaction mixture, upon leaving the preheater 17, enters the tower 1 through a line 18 partially surrounded by the pipe 4 and of such a' length as to require only a short ilow to the tower 1. Sight glasses, such as 19, pressure gauges, such as 20, thermometers, such as 2l, and outlets, such as 22,'may be provided where necessary as is well known. The -line 23 may be used for emptying the still 3 by suction.

Assuming that the tank 11 contains a'batch of the quinone reaction mixture, the recirculation of this mixture is started through the line 14 by means of the pump 13. The recirculation of the suspension of iron dust 'in water in the tank 7 is also commenced through the line 8 the eductor 5 and the line 6. Steam is then blown through the various llines provided for that purpose, the direct steam injected into the still 3 rising through the tower 1, the line 4-and the eductor 5, so that all portions of. the equipment are brought up to the approximate working temperature desired. A. small but steady stream `of the quinone reaction mixture is thon withdrawn from the line 14 and forced through the 'preheater 17 wherein it is rapidly brought to a temperature of approximately 100 C. yand is permitted to flow through the line 18 into the tower 1 wherein it trickles down over the coke packing for its intimate Contact with the steam rising through the tower 1, line 4, etc. The tower 1 may be from 8 to 10 ft. in height to permit complete va- 'porization vofthe uinone from the reactionl When t e residual quinone reacmixture. tlon mixture reaches the bottom of the tower 1, it is continually volatilized by the direct and indirect steam applied thereto thereby generating further steam to assist the process. 1t is not necessary that any of the sulfuric ac id contained ,in the quinone reaction mixture be carried over into the line 6 although a certain portion of this sulfuric acid may pass over as vapor and mingle with the quinone and steam vapor to assist in the reduction reaction which takes place at the eductor 5 and in the line 6. When the reduction of the quinone is complete and the reaction mixture contained in the tank 7 is more or less'saturated with hydroquinone, the solution maybe withdrawn from the tank 7 through the line 22 and thence conducted to the filtration and crystallization steps which are carried out in a, well known manner.

Although we do not wish to limit ourselves `by any specific examples of the constituents employed in producing the reactions above referred to (as these are all well known to those skilled in the art) it may be noted that in the production of the quinone, we may employ, in parts by weight, approximately 37 parts of man anese dioxide, 64 parts of 93% sulfuric acid, 13 parts of technicalaniline, and 224 parts of water, which mixture may 'be thoroughly stirred for a 20 hourreaction time at a temperature which may be maintained at 0 to 5 Cf With this quinone reaction. mixture we have found that approximately- 10 parts'of iron dust should be employed, which is, of course, an excess thereof to insure complete reduction of the quinone. This amount of iron dust -may be conveniently suspended in approximately parts of water which is sufficient to eompletely dissolve all the hydroquinone formed without hav-ing too great an ,excess of water to hamper the crystallizationl step. We'

mayV also employ, in parts by weight,'ap

proximately 75 parts of sodium dichromate, 200 parts of sulfuric acid, 25 parts' of v aniline and 900 parts of Water. With these materials and proportions, approximatelyy 20 'parts of iron dust 'and 160 parts of Water may be employed in reducing` the quinone.

It will be noted, therefore, that `our invention actually constitutes the combination of two steps which themselves are separately new, namely, on the one hand we have discovered that quinone may be steam distilledl from its reaction mixture, and on the other hand that by the intermingling of quinone in the vapor state (either 'with or without an acid radical) with a suspension of iron dust in water, a rapid and substantially complete reduction of the lquinone will take place. When these two steps are combined,

as heretofore indicated, a novel method for the production of hydroquinone results whichis continuous insofar as each charge or batch ofthe quinone reaction mixtureis concerned. Y

Obviously, various equivalents in the nature of equipment might be employed to carry out the spirit as well as the letter of our invention. For instance, various'"forms of towers might be employed for obtaining an intimate contact of the steam with the quinone. reaction mixture', and equipment of means for carrying out our invention shall, when carrying out our invention or the steps thereof, be considered to come within the scope of the claims appended hereto.

What We claim as our invention land desire to be 'secured by Letters Patent, is:

1. The process of producing hydroquinone which comprises Vaporizing quinone-from a solution containing it and intermingling the quinone vapors with a stream of Water having iron dust suspended therein.

2. The process of producing hydroquinone which comprises vaporizing quinone from a reaction mixture containing it and intermingling the quinone vapors with a stream of Water havingiron dust Suspended therein.

. 3. The process of producing hydroquinone which comprises vaporizing quinone from a reaction mixture containing it and 'intere mingling the quinone vapors with a re-circulated stream of Water having iron dust suspended therein.

4. The process of producing hydroquinone .intermingling the quinone vapors with a rewhich comprises vaporizing quinone from a solution containing itby passing thersaid solution countercurrcnt to a current of steam and intermingling the quinone and steam vapors with a stream of Water having iron dust suspended therein.

5. The process of producing hydroquinone which comprises vaporizing quinone from a solution containing it by passing the said solution countercurrent to a current of steam and intermingling the quinone and steam vapors with a re-.circulated stream of Water having iron dust suspended therein.

6. The process'of producing hydroquinone which comprises vaporizing quinone from a solution containing it by means of acurrent of steam and thereupon Without exposure to lan oxidizing atmosphere interminging the quinone and steam vapors With a re-circulated stream of Water having iron dust suspended therein.

4 7 The process of producing hydroquinone which comprises vaporizing quinone from a solution containing itA by rapidly preheating the said solution to approximately V100 C. passing the said solution countercurrent to a current of steam and intermingling the quinone and steam vapors with a stream of Water having iron dust suspended therein.

8. The process of producing hydroquinone which comprises vaporizing-quinone from a lsolution containing it by rapidly preheating the said solution to approximately 100 C., passing the said solution countercurrent to a currentof jsteam and intermingling Athe quinone and steam vapors'with a re-circulated stream of Water having iron dust suspend- 'ed therein.v v

A9. Ther process' of producing hydroquinone Which comprises intermingling quinone vapors With Water which has iron dust ysuspended therein.

10. The process of producing hydroquinone which comprises interminglin quinone vapors with a stream of Water Whic has iron dust suspended therein.

i 1l. The process of producing hydroquinone which comprises intermingling quinone vapors with 'a refcirculated stream of Water which has iron dust suspended therein.v

12. A process of producing hydroquinone which comprises vaporizing quinone from a solution containing it in an atmosphere free from .reactive gases and thereupon inter- A mingling the quinone vapors with areducing 13. A process of producing hydroquinone which comprises vaporizing quinone from a reaction mixture containing it in an atmosphere free from reactive gases and thereupon circulatedstream of reducing material.

14. A process of producing hydroquinone Which'comprises vaporizing 'quinone from a 1 solution containi. Agit by passing the said so- 4 memes@ lution counter-current to e current of seam and thereupon intermingling the quinone and steam vapors with e reducing agent.

15. The process of producing hydroquinone which comprises vaporizing quinone in un atmosphere free from reacting gases and thereupon intermingling the quinone vapors With a reducing agent.

Signed at Passaic Junction, N. J., this 13th day of May 1929.

HAROLD VON BEAMER. JOHN W. ZABRISKE.

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